WO2011155546A1 - Alkyl-modified vinyl alcohol polymer, and composition, thickener, coating material for paper, coated paper, adhesive and film that contain same - Google Patents
Alkyl-modified vinyl alcohol polymer, and composition, thickener, coating material for paper, coated paper, adhesive and film that contain same Download PDFInfo
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- WO2011155546A1 WO2011155546A1 PCT/JP2011/063182 JP2011063182W WO2011155546A1 WO 2011155546 A1 WO2011155546 A1 WO 2011155546A1 JP 2011063182 W JP2011063182 W JP 2011063182W WO 2011155546 A1 WO2011155546 A1 WO 2011155546A1
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- pva
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- 0 CCC(C)(*)C(N*)=O Chemical compound CCC(C)(*)C(N*)=O 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F120/00—Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F120/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F120/10—Esters
- C08F120/40—Esters of unsaturated alcohols, e.g. allyl (meth)acrylate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F16/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical
- C08F16/02—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical by an alcohol radical
- C08F16/04—Acyclic compounds
- C08F16/06—Polyvinyl alcohol ; Vinyl alcohol
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F218/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid
- C08F218/02—Esters of monocarboxylic acids
- C08F218/04—Vinyl esters
- C08F218/08—Vinyl acetate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/12—Hydrolysis
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L29/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical; Compositions of hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Compositions of derivatives of such polymers
- C08L29/02—Homopolymers or copolymers of unsaturated alcohols
- C08L29/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J129/00—Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Adhesives based on hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Adhesives based on derivatives of such polymers
- C09J129/02—Homopolymers or copolymers of unsaturated alcohols
- C09J129/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/44—Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
- D21H19/56—Macromolecular organic compounds or oligomers thereof obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H19/60—Polyalkenylalcohols; Polyalkenylethers; Polyalkenylesters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/3188—Next to cellulosic
- Y10T428/31895—Paper or wood
Definitions
- alkyl-modified PVA into which an alkyl group is introduced is known to exhibit an alkyl group (hydrophobic group) interaction in an aqueous solvent and increase the viscosity (Japanese Patent Laid-Open No. 55-47256). See the official gazette).
- the alkyl-modified PVA increases in viscosity as the alkyl group content increases. However, if the alkyl group content is too high, water solubility decreases.
- the alkyl-modified PVA of the present invention made to solve the above problems is
- the monomer unit (a) represented by the following general formula (I) is contained, the viscosity average polymerization degree is 200 or more and 5,000 or less, the saponification degree is 20 mol% or more and 99.99 mol% or less.
- the content rate of a body unit (a) is 0.05 mol% or more and 5 mol% or less.
- R 1 represents a linear or branched alkyl group having 8 to 29 carbon atoms.
- R 2 represents a hydrogen atom or an alkyl group having 1 to 8 carbon atoms.
- R 1 in the above formula (I) is preferably a linear or branched alkyl group having 15 to 26 carbon atoms.
- R 1 by using a long-chain alkyl group for R 1 , the above-described thickening and water resistance can be further enhanced.
- the composition of the present invention contains the alkyl-modified PVA. Since the composition contains the alkyl-modified PVA of the present invention, it can be suitably used as a thickener, a paper coating agent, an adhesive, a film, a paint, a binder, a fiber paste, and the like.
- the contact angle of the film with water is preferably 70 ° or more.
- the film can exhibit more excellent surface water repellency by having such a high contact angle.
- R 1 represents a linear or branched alkyl group having 8 to 29 carbon atoms.
- R 2 represents a hydrogen atom or an alkyl group having 1 to 8 carbon atoms.
- the R 1 and R 2 may have a substituent such as a halogen atom as long as the effect of the present invention is not impaired, but preferably does not have these substituents. .
- the content of the monomer unit (b) having a carboxyl group in the alkyl-modified PVA is preferably less than 0.1 mol%, and more preferably 0.01 mol% or less.
- the content of the monomer unit (b) is 0.1 mol% or more, the adhesiveness, water resistance, storage stability, strength when formed into a coating film, or the like is decreased or hydrophilic when formed into a film. May increase and the contact angle may decrease.
- the content rate of this monomer unit (b) is a content rate of this monomer unit (b) in all the structural units which comprise alkyl-modified PVA, and monomer unit (a) mentioned above Similarly to the content ratio, it can be determined from proton NMR.
- the saponification degree of the alkyl-modified PVA is a value that can be measured according to JIS-K6726.
- the unsaturated monomer represented by the above formula (II) include N-octylacrylamide, N-decylacrylamide, N-dodecylacrylamide, N-octadecylacrylamide, N-hexacosylacrylamide, and N-octyl.
- Examples include methacrylamide, N-decyl methacrylamide, N-dodecyl methacrylamide, N-octadecyl methacrylamide, N-hexacosyl methacrylamide and the like.
- Aldehydes such as acetaldehyde and propionaldehyde
- Ketones such as acetone and methyl ethyl ketone
- Mercaptans such as 2-hydroxyethanethiol
- Halogenated hydrocarbons such as trichlorethylene and perchlorethylene
- phosphinic acid salts such as sodium phosphinate monohydrate, among which aldehydes and ketones are preferably used.
- azo initiators As the initiator used for copolymerization, conventionally known azo initiators, peroxide initiators, redox initiators and the like are appropriately selected according to the polymerization method.
- the azo initiator include 2,2′-azobisisobutyronitrile, 2,2′-azobis (2,4-dimethylvaleronitrile), 2,2′-azobis (4-methoxy-2,4- Dimethyl valeronitrile) and the like
- peroxide initiators include perisopropyl compounds such as diisopropyl peroxydicarbonate, di-2-ethylhexyl peroxydicarbonate, diethoxyethyl peroxydicarbonate; t-butyl Perester compounds such as peroxyneodecanate, ⁇ -cumylperoxyneodecanate, and t-butylperoxydecanate; acetylcyclohexylsulfonyl peroxide; 2,4,4-trimethyl
- the concentration of the alkyl-modified PVA in the liquid composition is not particularly limited.
- the concentration can be 1% by mass or more and 10% by mass or less.
- the concentration can be relatively high.
- the liquid composition may include water and oil in addition to the alkyl-modified PVA.
- the composition has a high viscosity and is excellent in storage stability.
- the oil is usually present in an emulsion state dispersed in water.
- Such dispersions include aqueous polyacrylate dispersions, aqueous dispersions of olefinically unsaturated monomers alone or copolymers, aqueous polyvinyl acetate dispersions, aqueous polyurethane dispersions, aqueous polyester dispersions. And existing aqueous emulsion dispersions.
- the thickener of this invention contains the said alkyl modified PVA, it can exhibit the outstanding thickening.
- the amount of the alkyl-modified PVA is preferably 1 to 50 parts by mass, more preferably 3 to 30 parts by mass with respect to 100 parts by mass of the solvent.
- Such a liquid thickener is produced by adding the alkyl-modified PVA to water or a water-containing solvent and mixing them by heating.
- liquid thickener various plasticizers, surfactants, antifoaming agents, ultraviolet absorbers and the like may be blended as long as the effects of the present invention are not impaired.
- the filler examples include kaolin, clay, calcined clay, calcium carbonate, titanium oxide, diatomaceous earth, aluminum oxide, aluminum hydroxide, synthetic aluminum silicate, synthetic magnesium silicate, polystyrene fine particles, polyvinyl acetate fine particles, urea- Formalin resin fine particles, precipitated silica, gel silica, silica synthesized by gas phase method (hereinafter referred to as gas phase method silica), colloidal silica, colloidal alumina, pseudoboehmite, talc, zeolite, alumina, zinc oxide, satin Examples include white and organic pigments.
- the solid content concentration in the paper coating agent is not particularly limited and can be appropriately adjusted according to the use.
- the mass content is preferably 1% by mass to 65% by mass, and preferably 1% by mass. % To 40% by mass is more preferable, 1% to 20% by mass is more preferable, and 2% to 15% by mass is particularly preferable.
- the adhesive of the present invention contains the alkyl-modified PVA.
- the adhesive is usually an aqueous solution of the alkyl-modified PVA and may contain other additives.
- examples of the diene monomer include butadiene, isoprene, chloroprene and the like.
- the adhesive further contains a filler, thereby reducing the load during drying due to an increase in solid content and improving the strength and hardness after bonding.
- Inorganic fillers such as kaolinite, halloysite, pyroferrite or sericite clay, heavy, light or surface treated calcium carbonate, aluminum hydroxide, aluminum oxide, gypsum, talc, titanium oxide;
- organic fillers such as starch, oxidized starch, wheat flour and wood flour.
- various clays and various starches can be suitably used.
- the film contains various other water-soluble polymers such as various known PVA, starch, carboxymethylcellulose, methylcellulose, hydroxymethylcellulose, hydroxyethylcellulose, hydroxypropylmethylcellulose, etc., as long as the effects of the present invention are not impaired. You may do it.
- the blending amount of these other water-soluble polymers in the film is preferably 50 parts by mass or less with respect to 100 parts by mass of the alkyl-modified PVA.
- the obtained PVA (alkyl-modified PVA and non-modified PVA) was evaluated according to the following method.
- Modification rate The content of the monomer unit (a) represented by the formula (I) in PVA (hereinafter also referred to as “alkyl modification rate”) and the content of the monomer unit (b) having a carboxyl group (hereinafter, Each modification rate including “itaconic acid modification rate” was determined according to the above-described method using proton NMR.
- Pure content (%) ⁇ mass of PVA dried at 105 ° C. for 3 hours (g) / mass of PVA before drying (g) ⁇ ⁇ 100
- Insoluble content (%) ⁇ a (g) / 4 (g) ⁇ ⁇ ⁇ 100 / pure content (%) ⁇ ⁇ 100
- the insoluble content (%) calculated according to the above formula was determined according to the following criteria.
- the gel-like material was pulverized with a pulverizer and allowed to stand at 40 ° C. for 1 hour to allow saponification to proceed. Then, 500 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of neutralization using a phenolphthalein indicator, the mixture was filtered to obtain a white solid. To this white solid, 2,000 g of methanol was added, and the mixture was left to wash at room temperature for 3 hours. This washing operation was repeated three times, and then the white solid obtained by centrifugal drainage was left in a dryer at 65 ° C. for 2 days to obtain alkyl-modified PVA (PVA1).
- PVA1 alkyl-modified PVA
- Examples 2 to 15 and Comparative Examples 1 to 5 (Production of PVA 2 to 15 and PVA i to v) Charge amount of vinyl acetate and methanol, polymerization conditions such as kind and addition amount of unsaturated monomer having alkyl group used during polymerization, concentration of alkyl-modified PVAc during saponification, molar ratio of sodium hydroxide to vinyl acetate unit Various alkyl-modified PVAs (PVA2 to 15 and PVAi to v) were produced in the same manner as in Example 1 except that the saponification conditions such as the above were changed as shown in Table 1.
- the gel-like material was pulverized with a pulverizer and allowed to stand at 40 ° C. for 1 hour to allow saponification to proceed. Then, 500 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of neutralization using a phenolphthalein indicator, the mixture was filtered to obtain a white solid. To this white solid, 2,000 g of methanol was added, and the mixture was left to wash at room temperature for 3 hours. This washing operation was repeated three times, and then the white solid obtained by centrifugal drainage was left in a dryer at 65 ° C. for 2 days to obtain unmodified PVA (PVAviii).
- the degree of polymerization, modification rate, degree of saponification, water solubility, and water resistance of the obtained PVA were evaluated by the above methods. The evaluation results are shown in Table 1.
- Thickening thickening test of ethylene-vinyl acetate copolymer emulsion
- Examples 33 to 48 and Comparative Examples 17 to 24 (paper coating agent) Using the obtained PVA, paper coating agents for Examples 33 to 48 and Comparative Examples 17 to 24 were obtained by the following method. Each obtained paper coating agent was evaluated by the following methods. The evaluation results are shown in Table 3.
- the coating agent was applied to the surface of a commercially available thermal paper (manufactured by KOKUYO) with a wire bar No. After hand-painting using 60 (manufactured by ETO), the coated surface was dried at 50 ° C. for 1 hour using a hot air dryer. Next, the dried thermal paper is left in a room adjusted to 20 ° C. and 65% RH for 3 hours to determine the characteristics (water resistance and blocking resistance) of the thermal paper overcoat layer formed by the coating agent. It was set as the sample for evaluation.
- Example 74 An adhesive was prepared in the same manner as in Example 66 except that the PVA16 aqueous solution obtained in Example 64 was used instead of the PVA1 aqueous solution (the solid content mass ratio of PVA16 and PVAc was 100: 400). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
- Example 71 In place of the methyl methacrylate / n-butyl acrylate copolymer (ACR) emulsion, 29 ethylene-vinyl acetate copolymer (VAE) emulsion (OM-4200NT, solid content concentration 55.0%, manufactured by Kuraray Co., Ltd.) An adhesive was prepared in the same manner as in Example 70 except that 0.0 part was used (the solid content mass ratio of PVA1, VAE and clay was 100: 400: 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
- Example 72 Instead of methyl methacrylate / n-butyl acrylate copolymer (ACR) emulsion, styrene-butadiene copolymer (SBR) emulsion (Nalstar SR-107, solid content concentration 48.0%, manufactured by Nippon A & L Co., Ltd.) The same operation as in Example 70 was performed except that 33.3 parts were used to prepare an adhesive (the solid content mass ratio of PVA1, SBR, and clay was 100: 400: 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
- ACR methyl methacrylate / n-butyl acrylate copolymer
- SBR styrene-butadiene copolymer
- the adhesive of the present invention is excellent in initial adhesiveness and storage stability. Furthermore, the saponification degree of the alkyl-modified PVA to be used, the content of the monomer unit (a) represented by the general formula (I) (alkyl modification rate), the content of the monomer unit (b) having a carboxyl group It can be seen that by adjusting the rate (itaconic acid modification rate) and the like, excellent water-resistant adhesiveness can also be exhibited.
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Abstract
Description
下記一般式(I)で表される単量体単位(a)を含有し、粘度平均重合度が200以上5,000以下、けん化度が20モル%以上99.99モル%以下、上記単量体単位(a)の含有率が0.05モル%以上5モル%以下である。
The monomer unit (a) represented by the following general formula (I) is contained, the viscosity average polymerization degree is 200 or more and 5,000 or less, the saponification degree is 20 mol% or more and 99.99 mol% or less. The content rate of a body unit (a) is 0.05 mol% or more and 5 mol% or less.
当該アルキル変性PVAは、下記一般式(I)で表される単量体単位(a)を含有する。すなわち、当該アルキル変性PVAは、上記単量体単位(a)と、ビニルアルコール単量体単位(-CH2-CHOH-)との共重合体であり、さらに他の単量体単位を有していてもよい。 <Alkyl-modified PVA>
The alkyl-modified PVA contains a monomer unit (a) represented by the following general formula (I). That is, the alkyl-modified PVA is a copolymer of the monomer unit (a) and a vinyl alcohol monomer unit (—CH 2 —CHOH—), and further has other monomer units. It may be.
S(モル%)
={(βのプロトン数/3)/(αのプロトン数+(βのプロトン数/3))}×100 In this case, for example, when the alkyl-modified monomer unit other than the monomer unit (a) is not included, R 1 is linear, and R 2 is a hydrogen atom, the calculation is performed by the following method. it can. That is, the peak α (4.7 to 5.2 ppm) derived from the main chain methine of the alkyl-modified vinyl ester polymer and the peak β (0.8 to 1.0 ppm) derived from the terminal methyl group of the alkyl group R 1 From the above, the content S of the monomer unit (a) is calculated using the following formula.
S (mol%)
= {(Number of protons of β / 3) / (number of protons of α + (number of protons of β / 3))} × 100
P=([η]×103/8.29)(1/0.62) This viscosity average degree of polymerization (P) is measured according to JIS-K6726. That is, after re-saponifying and purifying the alkyl-modified PVA, it is obtained by the following formula from the intrinsic viscosity [η] (unit: deciliter / g) measured in water at 30 ° C.
P = ([η] × 10 3 /8.29) (1 / 0.62)
当該アルキル変性PVAを製造する方法は特に制限されないが、下記一般式(II)で表される不飽和単量体とビニルエステル系単量体との共重合を行い、得られたアルキル変性ビニルエステル系重合体をけん化する方法が好ましい。ここで、上記の共重合はアルコール系溶媒中又は無溶媒で行うことが好適である。 <Method for producing alkyl-modified PVA>
The method for producing the alkyl-modified PVA is not particularly limited, but the alkyl-modified vinyl ester obtained by copolymerizing an unsaturated monomer represented by the following general formula (II) and a vinyl ester monomer. A method of saponifying the polymer is preferred. Here, the above copolymerization is preferably performed in an alcohol solvent or without a solvent.
エチレン、プロピレン、n-ブテン、イソブチレン等のα-オレフィン;
メチルビニルエーテル、エチルビニルエーテル、n-プロピルビニルエーテル、i-プロピルビニルエーテル、n-ブチルビニルエーテル、i-ブチルビニルエーテル、t-ブチルビニルエーテル、2,3-ジアセトキシ-1-ビニルオキシプロパン等のビニルエーテル類;
アクリロニトリル、メタクリロニトリル等のニトリル類;
塩化ビニル、フッ化ビニル等のハロゲン化ビニル類;
塩化ビニリデン、フッ化ビニリデン等のハロゲン化ビニリデン類;
酢酸アリル、2,3-ジアセトキシ-1-アリルオキシプロパン、塩化アリル等のアリル化合物;
ビニルトリメトキシシラン等のビニルシリル化合物;
酢酸イソプロペニル
等が挙げられる。 When the unsaturated monomer represented by the general formula (II) and the vinyl ester monomer are copolymerized, other monomers may be copolymerized within a range not impairing the gist of the present invention. Examples of monomers that can be used include:
Α-olefins such as ethylene, propylene, n-butene and isobutylene;
Vinyl ethers such as methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, i-propyl vinyl ether, n-butyl vinyl ether, i-butyl vinyl ether, t-butyl vinyl ether, 2,3-diacetoxy-1-vinyloxypropane;
Nitriles such as acrylonitrile and methacrylonitrile;
Vinyl halides such as vinyl chloride and vinyl fluoride;
Vinylidene halides such as vinylidene chloride and vinylidene fluoride;
Allyl compounds such as allyl acetate, 2,3-diacetoxy-1-allyloxypropane, allyl chloride;
Vinylsilyl compounds such as vinyltrimethoxysilane;
And isopropenyl acetate.
アセトアルデヒド、プロピオンアルデヒド等のアルデヒド類;
アセトン、メチルエチルケトン等のケトン類;
2-ヒドロキシエタンチオール等のメルカプタン類;
トリクロロエチレン、パークロロエチレン等のハロゲン化炭化水素類;
ホスフィン酸ナトリウム1水和物等のホスフィン酸塩類
等が挙げられ、これらの中でもアルデヒド類およびケトン類が好適に用いられる。 In addition, in the copolymerization of the unsaturated monomer represented by the general formula (II) and the vinyl ester monomer, the purpose of the present invention is to adjust the degree of polymerization of the obtained copolymer. Copolymerization may be carried out in the presence of a chain transfer agent within a range that does not impair. As this chain transfer agent,
Aldehydes such as acetaldehyde and propionaldehyde;
Ketones such as acetone and methyl ethyl ketone;
Mercaptans such as 2-hydroxyethanethiol;
Halogenated hydrocarbons such as trichlorethylene and perchlorethylene;
Examples thereof include phosphinic acid salts such as sodium phosphinate monohydrate, among which aldehydes and ketones are preferably used.
本発明の組成物は、当該アルキル変性PVAを含むものである。当該組成物は、当該アルキル変性PVA、溶媒等を含む液体状のものであってもよいし、当該液体状の組成物が乾燥等により硬化した固体状のものであってもよい。なお、後に詳述する、増粘剤、紙用塗工剤やそれから得られる塗膜、接着剤及びフィルムも当該組成物に含まれる。以下、当該組成物が、液体状である場合について説明する。 <Composition>
The composition of the present invention contains the alkyl-modified PVA. The composition may be a liquid containing the alkyl-modified PVA, a solvent or the like, or may be a solid obtained by curing the liquid composition by drying or the like. In addition, the thickener, paper coating agent, and the coating film obtained from it, an adhesive agent, and a film which are explained in full detail later are also contained in the said composition. Hereinafter, the case where the composition is in a liquid form will be described.
本発明の増粘剤は、当該アルキル変性PVAを含むため、優れた増粘性を発揮することができる。 <Thickener>
Since the thickener of this invention contains the said alkyl modified PVA, it can exhibit the outstanding thickening.
本発明の紙用塗工剤は、当該アルキル変性PVAを含有する。当該紙用塗工剤は、通常、当該アルキル変性PVAの水溶液であり、その他の溶媒や添加剤が含まれていてもよい。 <Paper coating agent>
The paper coating agent of the present invention contains the alkyl-modified PVA. The paper coating agent is usually an aqueous solution of the alkyl-modified PVA, and may contain other solvents and additives.
本発明の塗工紙は、上記紙用塗工剤が紙表面に塗工されてなるものである。当該塗工紙は、上記紙用塗工剤が表面に塗工されているため、表面の強度及び耐水性に優れる。当該塗工紙は、公知の方法で製造することができる。当該塗工紙は、例えば感熱紙、インクジェット記録紙、剥離紙原紙等として好適に用いることができる。 <Coated paper>
The coated paper of the present invention is obtained by coating the paper coating agent on the paper surface. The coated paper is excellent in surface strength and water resistance since the paper coating agent is coated on the surface. The coated paper can be produced by a known method. The coated paper can be suitably used as, for example, thermal paper, ink jet recording paper, release paper base paper, and the like.
本発明の接着剤は、当該アルキル変性PVAを含有する。当該接着剤は、通常、当該アルキル変性PVAの水溶液であり、その他の添加剤等が含まれていてもよい。 <Adhesive>
The adhesive of the present invention contains the alkyl-modified PVA. The adhesive is usually an aqueous solution of the alkyl-modified PVA and may contain other additives.
酢酸ビニル重合体、酢酸ビニル-エチレン共重合体、酢酸ビニル-バーサチック酸ビニル共重合体、酢酸ビニル-(メタ)アクリル酸エステル共重合体等の酢酸ビニル系エマルジョン;
メタクリル酸メチル/アクリル酸n-ブチル共重合体等の(メタ)アクリル酸エステル系エマルジョン;
スチレン系エマルジョン;
スチレン-ブタジエン共重合体、メタクリル酸メチルーブタジエン共重合体等のブタジエン系エマルジョン
等を挙げることができる。 As such a polymer emulsion, specifically,
Vinyl acetate emulsions such as vinyl acetate polymer, vinyl acetate-ethylene copolymer, vinyl acetate-vinyl versatate copolymer, vinyl acetate- (meth) acrylate copolymer;
(Meth) acrylate emulsions such as methyl methacrylate / n-butyl acrylate copolymer;
Styrene emulsion;
Examples thereof include butadiene-based emulsions such as styrene-butadiene copolymer and methyl methacrylate-butadiene copolymer.
カオリナイト、ハロイサイト、パイロフェライト又はセリサイト等のクレー、重質、軽質又は表面処理された炭酸カルシウム、水酸化アルミニウム、酸化アルミニウム、石膏類、タルク、酸化チタン等の無機系フィラー;
澱粉、酸化澱粉、小麦粉、木紛等の有機系フィラー
等を挙げることができる。これらの中でも、各種クレー及び各種澱粉が好適に使用できる。 As the filler,
Inorganic fillers such as kaolinite, halloysite, pyroferrite or sericite clay, heavy, light or surface treated calcium carbonate, aluminum hydroxide, aluminum oxide, gypsum, talc, titanium oxide;
Examples thereof include organic fillers such as starch, oxidized starch, wheat flour and wood flour. Among these, various clays and various starches can be suitably used.
本発明のフィルムは、当該アルキル変性PVAを含むものである。当該フィルムは、当該アルキル変性PVAを含むため、高い表面撥水性を有することができる。
当該フィルムにおける当該アルキル変性PVAの含有率としては、通常50質量%以上であり、90質量%以上がさらに好ましい。当該アルキル変性PVAの含有率を上記範囲とすることで、当該フィルムの撥水性を効果的に発現させることができる。 <Film>
The film of the present invention contains the alkyl-modified PVA. Since the film contains the alkyl-modified PVA, the film can have high surface water repellency.
The content of the alkyl-modified PVA in the film is usually 50% by mass or more, and more preferably 90% by mass or more. By setting the content of the alkyl-modified PVA in the above range, the water repellency of the film can be effectively expressed.
(1)含水状態の当該アルキル変性PVAを溶融押出法により製膜する方法、
(2)当該アルキル変性PVAを溶媒に溶解した製膜原液を使用し、流延製膜法、湿式製膜法(貧溶媒中への吐出)、ゲル製膜法(溶液を一旦冷却しゲル化した後、溶媒を抽出除去し、フィルムを得る方法)及びこれらの組み合わせによる方法
等を挙げることができる。
これらの製造方法の中でも、流延製膜法及び溶融押出製膜法が、良好なフィルムを得られることから好ましい。 As a manufacturing method of the film, for example,
(1) A method of forming a film of the water-containing alkyl-modified PVA by a melt extrusion method,
(2) Using a film-forming stock solution in which the alkyl-modified PVA is dissolved in a solvent, a casting film-forming method, a wet film-forming method (discharging into a poor solvent), a gel film-forming method (cooling the solution once to gelation) Then, the solvent is extracted and removed to obtain a film) and a combination thereof.
Among these production methods, the casting film forming method and the melt extrusion film forming method are preferable because a good film can be obtained.
PVAにおける式(I)で表される単量体単位(a)の含有率(以下、「アルキル変性率」ともいう。)及びカルボキシル基を有する単量体単位(b)の含有率(以下、「イタコン酸変性率」ともいう。)を含む各変性率は、上述した、プロトンNMRを用いた方法に準じて求めた。 [Modification rate]
The content of the monomer unit (a) represented by the formula (I) in PVA (hereinafter also referred to as “alkyl modification rate”) and the content of the monomer unit (b) having a carboxyl group (hereinafter, Each modification rate including “itaconic acid modification rate” was determined according to the above-described method using proton NMR.
PVAの重合度は、JIS-K6726に記載の方法により求めた。 [Degree of polymerization]
The degree of polymerization of PVA was determined by the method described in JIS-K6726.
PVAのけん化度は、JIS-K6726に記載の方法により求めた。 [Saponification degree]
The degree of saponification of PVA was determined by the method described in JIS-K6726.
蒸留水96gに対してPVA4gを室温で加え、30分間撹拌した。得られたPVA水溶液を90℃まで昇温し、そのまま1時間撹拌した後、室温まで冷却し、105mmφの金網を用いて濾過した。濾過後、金網を105℃で3時間乾燥させ、デシケーター内で室温まで冷却した後に質量を測定して、濾過の前後で増加した金網の質量を求めた。濾過後に増加した金網の質量をa(g)とし、下記式に従って不溶解分(%)を算出した。なお、不溶解分を算出するのに用いた式において、純分(%)とは下記式を用いて求めた値である。
純分(%)={105℃で3時間乾燥させたPVAの質量(g)/乾燥前のPVAの質量(g)}×100
不溶解分(%)={a(g)/4(g)}×{100/純分(%)}×100
上記式に従って算出した不溶解分(%)を以下の基準にしたがって判定した。
A:0.01%未満
B:0.01%以上0.1%未満
C:0.1%以上0.5%未満
D:0.5%以上1.0%未満
E:1.0%以上 [Water soluble]
4 g of PVA was added to 96 g of distilled water at room temperature and stirred for 30 minutes. The obtained PVA aqueous solution was heated to 90 ° C., stirred as it was for 1 hour, cooled to room temperature, and filtered using a 105 mmφ wire mesh. After filtration, the wire mesh was dried at 105 ° C. for 3 hours, cooled to room temperature in a desiccator, the mass was measured, and the mass of the wire mesh increased before and after filtration was determined. The mass of the wire mesh increased after filtration was defined as a (g), and the insoluble content (%) was calculated according to the following formula. In the formula used to calculate the insoluble content, the pure content (%) is a value obtained using the following formula.
Pure content (%) = {mass of PVA dried at 105 ° C. for 3 hours (g) / mass of PVA before drying (g)} × 100
Insoluble content (%) = {a (g) / 4 (g)} × {100 / pure content (%)} × 100
The insoluble content (%) calculated according to the above formula was determined according to the following criteria.
A: Less than 0.01% B: 0.01% or more and less than 0.1% C: 0.1% or more and less than 0.5% D: 0.5% or more and less than 1.0% E: 1.0% or more
濃度4%のPVA水溶液を調製し、これを20℃でポリエチレンテレフタレート(PET)フィルム上に流延し、厚み40μmの皮膜を得た。得られた皮膜を縦5cm、横5cmの大きさに切り出して試験片を作製し、質量(質量A)を測定した。この試験片を20℃の蒸留水に24時間浸漬した後、回収し、表面に付着した水分をガーゼでふき取り、105℃で16時間乾燥した後、質量(質量B)を測定した。浸漬前の皮膜の含水率をC(質量%)とし、下記式に従って溶出率(%)を求め、以下の基準にしたがって判定した。浸漬前の皮膜の含水率は、別途切り出した浸漬前の皮膜を105℃、4時間で乾燥し、あらかじめ求めた。
溶出率(%)=[1-B/{(1-C/100)×A}]×100
A:5.0%未満
B:5.0%以上10.0%未満
C:10.0%以上20.0%未満
D:20.0%以上、または、試験片が溶解し、回収できなかった。 [Water resistance of coating made of PVA]
A PVA aqueous solution having a concentration of 4% was prepared and cast on a polyethylene terephthalate (PET) film at 20 ° C. to obtain a film having a thickness of 40 μm. The obtained film was cut into a size of 5 cm in length and 5 cm in width to produce a test piece, and the mass (mass A) was measured. This test piece was immersed in distilled water at 20 ° C. for 24 hours and then collected, and moisture adhering to the surface was wiped off with gauze and dried at 105 ° C. for 16 hours, and then the mass (mass B) was measured. The water content of the film before immersion was C (mass%), the dissolution rate (%) was determined according to the following formula, and the determination was made according to the following criteria. The moisture content of the film before dipping was obtained in advance by drying the separately cut film before dipping at 105 ° C. for 4 hours.
Elution rate (%) = [1-B / {(1-C / 100) × A}] × 100
A: Less than 5.0% B: 5.0% or more and less than 10.0% C: 10.0% or more and less than 20.0% D: 20.0% or more, or the test piece is dissolved and cannot be recovered It was.
撹拌機、還流冷却管、窒素導入管、コモノマー滴下口及び開始剤の添加口を備えた3Lの反応器に、酢酸ビニル750g、メタノール250g及びN-オクタデシルメタクリルアミド1.1gを仕込み、窒素バブリングをしながら30分間系内を窒素置換した。また、ディレー溶液としてN-オクタデシルメタクリルアミドをメタノールに溶解して濃度5%としたコモノマー溶液を調製し、このコモノマー溶液を窒素ガスのバブリングにより窒素置換した。反応器の昇温を開始し、内温が60℃となったところで、2,2’-アゾビスイソブチロニトリル(AIBN)0.25gを添加し重合を開始した。上記反応器に、上記ディレー溶液を滴下して重合溶液中のモノマー組成が一定となるようにしながら、60℃で3時間重合した後、冷却して重合を停止した。重合を停止するまで加えたコモノマーの総量は4.8gであった。また重合停止時の固形分濃度は29.9%であった。続いて30℃、減圧下でメタノールを時々添加しながら未反応の酢酸ビニルモノマーの除去を行い、アルキル変性酢酸ビニル系重合体(アルキル変性PVAc)のメタノール溶液(濃度35%)を得た。さらに、これにメタノールを加えて調製したアルキル変性PVAcのメタノール溶液771.4g(溶液中のアルキル変性PVAcは200.0g)に、27.9gのアルカリ溶液(水酸化ナトリウムの10%メタノール溶液)を添加してけん化を行った。ここで、けん化溶液におけるアルキル変性PVAcの濃度は25%、アルキル変性PVAc中の酢酸ビニルユニットに対する水酸化ナトリウムのモル比は0.03であった。アルカリ溶液を添加後約1分でゲル状物が生成した。このゲル状物を粉砕器にて粉砕し、40℃で1時間放置してけん化を進行させた後、酢酸メチル500gを加えて残存するアルカリを中和した。フェノールフタレイン指示薬を用いて中和が終了したことを確認した後、濾別して白色固体を得た。この白色固体にメタノール2,000gを加えて室温で3時間放置洗浄した。この洗浄操作を3回繰り返した後、遠心脱液して得られた白色固体を乾燥機中65℃で2日間放置してアルキル変性PVA(PVA1)を得た。 Example 1 (Production of PVA1)
A 3 L reactor equipped with a stirrer, reflux condenser, nitrogen inlet, comonomer addition port and initiator addition port was charged with 750 g of vinyl acetate, 250 g of methanol and 1.1 g of N-octadecyl methacrylamide and subjected to nitrogen bubbling. Then, the system was purged with nitrogen for 30 minutes. Further, a comonomer solution having a concentration of 5% was prepared by dissolving N-octadecylmethacrylamide in methanol as a delay solution, and this comonomer solution was purged with nitrogen by bubbling nitrogen gas. The temperature of the reactor was increased, and when the internal temperature reached 60 ° C., 0.25 g of 2,2′-azobisisobutyronitrile (AIBN) was added to initiate polymerization. The delay solution was added dropwise to the reactor so that the monomer composition in the polymerization solution was constant, and polymerization was performed at 60 ° C. for 3 hours, followed by cooling to stop the polymerization. The total amount of comonomer added until the polymerization was stopped was 4.8 g. The solid content concentration when the polymerization was stopped was 29.9%. Subsequently, unreacted vinyl acetate monomer was removed while occasionally adding methanol under reduced pressure at 30 ° C. to obtain a methanol solution (concentration 35%) of an alkyl-modified vinyl acetate polymer (alkyl-modified PVAc). Further, 777.9 g of alkyl-modified PVAc methanol solution prepared by adding methanol (200.0 g of alkyl-modified PVAc in the solution) was added to 27.9 g of an alkali solution (sodium hydroxide in 10% methanol). Saponification was performed by adding. Here, the concentration of the alkyl-modified PVAc in the saponification solution was 25%, and the molar ratio of sodium hydroxide to the vinyl acetate unit in the alkyl-modified PVAc was 0.03. A gel was formed about 1 minute after the addition of the alkaline solution. The gel-like material was pulverized with a pulverizer and allowed to stand at 40 ° C. for 1 hour to allow saponification to proceed. Then, 500 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of neutralization using a phenolphthalein indicator, the mixture was filtered to obtain a white solid. To this white solid, 2,000 g of methanol was added, and the mixture was left to wash at room temperature for 3 hours. This washing operation was repeated three times, and then the white solid obtained by centrifugal drainage was left in a dryer at 65 ° C. for 2 days to obtain alkyl-modified PVA (PVA1).
酢酸ビニル及びメタノールの仕込み量、重合時に使用するアルキル基を有する不飽和単量体の種類や添加量等の重合条件、けん化時におけるアルキル変性PVAcの濃度、酢酸ビニルユニットに対する水酸化ナトリウムのモル比等のけん化条件を表1に示すように変更した以外は、実施例1と同様の方法により各種のアルキル変性PVA(PVA2~15及びPVAi~v)を製造した。 Examples 2 to 15 and Comparative Examples 1 to 5 (Production of PVA 2 to 15 and PVA i to v)
Charge amount of vinyl acetate and methanol, polymerization conditions such as kind and addition amount of unsaturated monomer having alkyl group used during polymerization, concentration of alkyl-modified PVAc during saponification, molar ratio of sodium hydroxide to vinyl acetate unit Various alkyl-modified PVAs (PVA2 to 15 and PVAi to v) were produced in the same manner as in Example 1 except that the saponification conditions such as the above were changed as shown in Table 1.
撹拌機、還流冷却管、窒素導入管、コモノマー滴下口及び開始剤の添加口を備えた3Lの反応器に、酢酸ビニル750g、メタノール250g、N-オクタデシルメタクリルアミド1.1g及びイタコン酸0.7gを仕込み、窒素バブリングをしながら30分間系内を窒素置換した。また、ディレー溶液として、N-オクタデシルメタクリルアミドをメタノールに溶解して濃度5%としたコモノマー溶液と、イタコン酸をメタノール溶液に溶解して濃度25%としたコモノマー溶液とを調製し、これらのコモノマー溶液を窒素ガスのバブリングにより窒素置換した。反応器の昇温を開始し、内温が60℃となったところで、2,2’-アゾビスイソブチロニトリル(AIBN)0.3gを添加し重合を開始した。上記ディレー溶液を滴下して重合溶液中のモノマー組成(酢酸ビニル、N-オクタデシルメタクリルアミド及びイタコン酸の比率)が一定となるようにしながら、60℃で3時間重合した後、冷却して重合を停止した。重合を停止するまで加えたN-オクタデシルメタクリルアミドの総量は4.8g、イタコン酸の総量は9.6gであった。また、重合停止時の固形分濃度は29.9%であった。続いて30℃、減圧下でメタノールを時々添加しながら未反応の酢酸ビニルモノマーの除去を行い、アルキル-イタコン酸変性酢酸ビニル系重合体(アルキル-イタコン酸変性PVAc)のメタノール溶液(濃度35%)を得た。さらに、これにメタノールを加えて調製したアルキル-イタコン酸変性PVAcのメタノール溶液706.9g(溶液中のアルキル-イタコン酸変性PVAcは200.0g)に、93.2gのアルカリ溶液(水酸化ナトリウムの10%メタノール溶液)を添加してけん化を行った。ここで、けん化溶液におけるアルキル-イタコン酸変性PVAcの濃度は25%、アルキル-イタコン酸変性PVAc中の酢酸ビニルユニットに対する水酸化ナトリウムのモル比は0.1であった。アルカリ溶液を添加後約1分でゲル状物が生成した。このゲル状物を粉砕器にて粉砕し、40℃で1時間放置してけん化を進行させた後、酢酸メチル500gを加えて残存するアルカリを中和した。フェノールフタレイン指示薬を用いて中和が終了したことを確認した後、濾別して白色固体を得た。この白色固体にメタノール2,000gを加えて室温で3時間放置洗浄した。この洗浄操作を3回繰り返した後、遠心脱液して得られた白色固体を乾燥機中65℃で2日間放置してアルキル-イタコン酸変性PVA(PVA16)を得た。 Example 16 (Production of PVA16)
In a 3 L reactor equipped with a stirrer, reflux condenser, nitrogen inlet, comonomer addition port and initiator addition port, 750 g of vinyl acetate, 250 g of methanol, 1.1 g of N-octadecylmethacrylamide and 0.7 g of itaconic acid The system was purged with nitrogen for 30 minutes while bubbling nitrogen. In addition, as a delay solution, a comonomer solution in which N-octadecylmethacrylamide was dissolved in methanol to a concentration of 5% and a comonomer solution in which itaconic acid was dissolved in a methanol solution to a concentration of 25% were prepared. The solution was purged with nitrogen by bubbling nitrogen gas. The temperature of the reactor was increased, and when the internal temperature reached 60 ° C., 0.3 g of 2,2′-azobisisobutyronitrile (AIBN) was added to initiate polymerization. The above delay solution was added dropwise to polymerize the monomer composition (ratio of vinyl acetate, N-octadecylmethacrylamide and itaconic acid) in the polymerization solution for 3 hours at 60 ° C., and then cooled to polymerize. Stopped. The total amount of N-octadecylmethacrylamide added until the polymerization was stopped was 4.8 g, and the total amount of itaconic acid was 9.6 g. Further, the solid content concentration at the time of termination of polymerization was 29.9%. Subsequently, unreacted vinyl acetate monomer was removed while occasionally adding methanol at 30 ° C. under reduced pressure to obtain a methanol solution of alkyl-itaconic acid-modified vinyl acetate polymer (alkyl-itaconic acid-modified PVAc) (concentration 35%). ) Furthermore, methanol was added to 706.9 g of an alkyl-itaconic acid-modified PVAc solution in methanol (200.0 g of alkyl-itaconic acid-modified PVAc in the solution), and 93.2 g of an alkaline solution (sodium hydroxide solution). 10% methanol solution) was added for saponification. Here, the concentration of alkyl-itaconic acid-modified PVAc in the saponification solution was 25%, and the molar ratio of sodium hydroxide to vinyl acetate units in the alkyl-itaconic acid-modified PVAc was 0.1. A gel was formed about 1 minute after the addition of the alkaline solution. The gel-like material was pulverized with a pulverizer and allowed to stand at 40 ° C. for 1 hour to allow saponification to proceed. Then, 500 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of neutralization using a phenolphthalein indicator, the mixture was filtered to obtain a white solid. To this white solid, 2,000 g of methanol was added, and the mixture was left to wash at room temperature for 3 hours. This washing operation was repeated three times, and then the white solid obtained by centrifugal deliquoring was left in a dryer at 65 ° C. for 2 days to obtain alkyl-itaconic acid-modified PVA (PVA16).
撹拌機、還流冷却管、窒素導入管及び開始剤の添加口を備えた3Lの反応器に、酢酸ビニル750g、メタノール250g及びオクタデシルビニルエーテル57.3gを仕込み、窒素バブリングをしながら30分間系内を窒素置換した。反応器の昇温を開始し、内温が60℃となったところで、2,2’-アゾビスイソブチロニトリル(AIBN)1.0gを添加し重合を開始した。60℃で2時間重合した後、冷却して重合を停止した。重合停止時の固形分濃度は30.4%であった。続いて30℃、減圧下でメタノールを時々添加しながら未反応の酢酸ビニルモノマーの除去を行い、アルキル変性酢酸ビニル系共重合体(アルキル変性PVAc)のメタノール溶液(濃度35%)を得た。さらに、これにメタノールを加えて調製したアルキル変性PVAcのメタノール溶液792.9g(溶液中のアルキル変性PVAcは200.0g)に、7.0gのアルカリ溶液(水酸化ナトリウムの10%メタノール溶液)を添加してけん化を行った。ここで、けん化溶液におけるアルキル変性PVAcの濃度は25%、アルキル変性PVAc中の酢酸ビニルユニットに対する水酸化ナトリウムのモル比は0.0075であった。アルカリ溶液を添加後約12分でゲル状物が生成した。このゲル状物を粉砕器にて粉砕し、40℃で1時間放置してけん化を進行させた後、酢酸メチル500gを加えて残存するアルカリを中和した。フェノールフタレイン指示薬を用いて中和が終了したことを確認した後、濾別して白色固体を得た。この白色固体にメタノール2,000gを加えて室温で3時間放置洗浄した。この洗浄操作を3回繰り返した後、遠心脱液して得られた白色固体を乾燥機中65℃で2日間放置してアルキル変性PVA(PVAvi)を得た。 Comparative Example 6 (Production of PVAvi)
A 3 L reactor equipped with a stirrer, a reflux condenser, a nitrogen inlet and an initiator addition port was charged with 750 g of vinyl acetate, 250 g of methanol and 57.3 g of octadecyl vinyl ether, and the system was circulated for 30 minutes while bubbling nitrogen. Replaced with nitrogen. The temperature of the reactor was increased, and when the internal temperature reached 60 ° C., 1.0 g of 2,2′-azobisisobutyronitrile (AIBN) was added to initiate polymerization. After polymerization at 60 ° C. for 2 hours, the polymerization was stopped by cooling. The solid content concentration when the polymerization was stopped was 30.4%. Subsequently, unreacted vinyl acetate monomer was removed while sometimes adding methanol under reduced pressure at 30 ° C. to obtain a methanol solution (concentration 35%) of an alkyl-modified vinyl acetate copolymer (alkyl-modified PVAc). Further, 79 g of an alkyl-modified PVAc methanol solution prepared by adding methanol to 792.9 g (200.0 g of the alkyl-modified PVAc in the solution) was added to 7.0 g of an alkali solution (10% sodium hydroxide in methanol solution). Saponification was performed by adding. Here, the concentration of the alkyl-modified PVAc in the saponification solution was 25%, and the molar ratio of sodium hydroxide to the vinyl acetate unit in the alkyl-modified PVAc was 0.0075. A gel-like material was formed about 12 minutes after the addition of the alkaline solution. The gel-like material was pulverized with a pulverizer and allowed to stand at 40 ° C. for 1 hour to allow saponification to proceed. Then, 500 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of neutralization using a phenolphthalein indicator, the mixture was filtered to obtain a white solid. To this white solid, 2,000 g of methanol was added, and the mixture was left to wash at room temperature for 3 hours. After this washing operation was repeated three times, the white solid obtained by centrifugal drainage was left in a dryer at 65 ° C. for 2 days to obtain alkyl-modified PVA (PVAvi).
アルキル基を有する不飽和単量体としてラウリルビニルエーテルを用いた以外は、比較例6と同様の方法によりアルキル変性PVA(PVAvii)を製造した。 Comparative Example 7 (Production of PVAvii)
An alkyl-modified PVA (PVAvii) was produced in the same manner as in Comparative Example 6 except that lauryl vinyl ether was used as the unsaturated monomer having an alkyl group.
撹拌機、還流冷却管、窒素導入管及び開始剤の添加口を備えた3Lの反応器に、酢酸ビニル900g及びメタノール100gを仕込み、窒素バブリングをしながら30分間系内を窒素置換した。反応器の昇温を開始し、内温が60℃となったところで、2,2’-アゾビスイソブチロニトリル(AIBN)0.25gを添加し重合を開始し、60℃で3時間重合した後、冷却して重合を停止した。重合停止時の固形分濃度は31.0%であった。続いて30℃、減圧下でメタノールを時々添加しながら未反応の酢酸ビニルモノマーの除去を行い、ポリ酢酸ビニル(PVAc)のメタノール溶液(濃度30%)を得た。さらに、これにメタノールを加えて調製したPVAcのメタノール溶液971.1g(溶液中のPVAcは200.0g)に、27.9gのアルカリ溶液(水酸化ナトリウムの10%メタノール溶液)を添加してけん化を行った。ここで、けん化溶液におけるPVAcの濃度は20%、PVAc中の酢酸ビニルユニットに対する水酸化ナトリウムのモル比は0.03であった。アルカリ溶液を添加後約1分でゲル状物が生成した。このゲル状物を粉砕器にて粉砕し、40℃で1時間放置してけん化を進行させた後、酢酸メチル500gを加えて残存するアルカリを中和した。フェノールフタレイン指示薬を用いて中和が終了したことを確認した後、濾別して白色固体を得た。この白色固体にメタノール2,000gを加えて室温で3時間放置洗浄した。この洗浄操作を3回繰り返した後、遠心脱液して得られた白色固体を乾燥機中65℃で2日間放置して無変性PVA(PVAviii)を得た。 Comparative Example 8 (Production of PVAviii)
900 g of vinyl acetate and 100 g of methanol were charged into a 3 L reactor equipped with a stirrer, reflux condenser, nitrogen inlet tube and initiator addition port, and the system was purged with nitrogen for 30 minutes while bubbling nitrogen. The temperature of the reactor was increased, and when the internal temperature reached 60 ° C., 0.25 g of 2,2′-azobisisobutyronitrile (AIBN) was added to start polymerization, and polymerization was performed at 60 ° C. for 3 hours. Then, the polymerization was stopped by cooling. The solid content concentration when the polymerization was stopped was 31.0%. Subsequently, unreacted vinyl acetate monomer was removed while sometimes adding methanol under reduced pressure at 30 ° C. to obtain a methanol solution (concentration 30%) of polyvinyl acetate (PVAc). Furthermore, 27.9 g of an alkaline solution (sodium hydroxide in 10% methanol) was added to 971.1 g of PVAc methanol solution prepared by adding methanol to this solution (200.0 g of PVAc in the solution) to saponify. Went. Here, the concentration of PVAc in the saponification solution was 20%, and the molar ratio of sodium hydroxide to vinyl acetate units in PVAc was 0.03. A gel was formed about 1 minute after the addition of the alkaline solution. The gel-like material was pulverized with a pulverizer and allowed to stand at 40 ° C. for 1 hour to allow saponification to proceed. Then, 500 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of neutralization using a phenolphthalein indicator, the mixture was filtered to obtain a white solid. To this white solid, 2,000 g of methanol was added, and the mixture was left to wash at room temperature for 3 hours. This washing operation was repeated three times, and then the white solid obtained by centrifugal drainage was left in a dryer at 65 ° C. for 2 days to obtain unmodified PVA (PVAviii).
2)アルキル変性PVAc中の酢酸ビニルユニットに対する水酸化ナトリウム(NaOH)のモル比。
3)酢酸ビニル、N-オクタデシルメタクリルアミド、イタコン酸を用いた重合を実施。
4)アルキル変性率/イタコン酸変性率
2) Molar ratio of sodium hydroxide (NaOH) to vinyl acetate units in alkyl-modified PVAc.
3) Polymerization using vinyl acetate, N-octadecylmethacrylamide and itaconic acid.
4) Alkyl modification rate / Itaconic acid modification rate
得られた各PVAを実施例17~32及び比較例9~16の増粘剤として用い、以下の評価を行った。また、この増粘剤(PVA)を含む組成物の評価を以下の方法にて行った。評価結果を表2に示す。 Examples 17 to 32 and Comparative Examples 9 to 16 (thickener and composition)
The obtained PVA was used as a thickener in Examples 17 to 32 and Comparative Examples 9 to 16, and the following evaluation was performed. Moreover, the following method evaluated the composition containing this thickener (PVA). The evaluation results are shown in Table 2.
上述と同様の方法で濃度4%のPVA水溶液を調製し、B型粘度計を用いてロータ回転数6rpmで温度が20℃における粘度を測定した。 [Thickening (viscosity of PVA aqueous solution)]
A PVA aqueous solution having a concentration of 4% was prepared by the same method as described above, and the viscosity at a temperature of 20 ° C. was measured at a rotor rotation speed of 6 rpm using a B-type viscometer.
エチレン-酢酸ビニル共重合体エマルジョン(株式会社クラレ製OM-4200NT、濃度55%)100部に濃度4%のPVA水溶液20.6部(PVAの固形分はエマルジョン固形分100部に対して1.5部)及び水2.4部を添加し、濃度45%のPVAとエマルジョンの混合溶液を作製し、B型粘度計を用いてロータ回転数6rpmで温度が20℃における粘度を測定し、以下の基準で判定した。
A:10,000mPa・s以上
B:5,000mPa・s以上10,000mPa・s未満
C:1,000mPa・s以上5,000mPa・s未満
D:500mPa・s以上1,000mPa・s未満
E:500mPa・s未満 [Thickening (thickening test of ethylene-vinyl acetate copolymer emulsion)]
100 parts of an ethylene-vinyl acetate copolymer emulsion (OM-4200NT manufactured by Kuraray Co., Ltd., concentration 55%) and 20.6 parts of a 4% concentration PVA aqueous solution (the solid content of PVA is 1. 5 parts) and 2.4 parts of water were added to prepare a mixed solution of PVA and emulsion having a concentration of 45%, and the viscosity at a temperature of 20 ° C. was measured at a rotor speed of 6 rpm using a B-type viscometer. Judged by the criteria of.
A: 10,000 mPa · s or more B: 5,000 mPa · s or more and less than 10,000 mPa · s C: 1,000 mPa · s or more and less than 5,000 mPa · s D: 500 mPa · s or more and less than 1,000 mPa · s E: <500 mPa · s
増粘試験に使用した溶液を50℃の乾燥機中に保管し、エマルジョン層と水層が分離するのに要した日数を観察し、以下の基準で判定した。
A:30日間以上
B:15日間以上30日間未満
C:7日間以上15日間未満
D:3日間以上7日間未満
E:3日間未満 [Storage stability of ethylene-vinyl acetate copolymer emulsion]
The solution used for the thickening test was stored in a dryer at 50 ° C., the number of days required for separation of the emulsion layer and the aqueous layer was observed, and judged according to the following criteria.
A: 30 days or more B: 15 days or more and less than 30 days C: 7 days or more and less than 15 days D: 3 days or more and less than 7 days E: Less than 3 days
2)粘度の測定限界は100,000mPa・s
3)酢酸ビニル、N-オクタデシルメタクリルアミド、イタコン酸を用いた重合を実施。
4)アルキル変性率/イタコン酸変性率
3) Polymerization using vinyl acetate, N-octadecylmethacrylamide and itaconic acid.
4) Alkyl modification rate / Itaconic acid modification rate
クラレ社製「ポバール」PVA-217で安定化されたPVAcエマルジョン(PVAc100部に対して、7.5部のPVA-217を添加)、上記PVA14を添加して、総固形分が35%、20℃、6rpmにおける粘度が10,000mPa・sの、フェノキシエタノールをPVAc100部に対して4部含有する水性エマルジョン接着剤を作製した。
米ツガ材に、上記水性エマルジョン接着剤を200g/m2塗布し、ただちに同種の米ツガ材を貼り合わせ、7kg/cm2の圧力で24時間圧締した。その後、解圧し、20℃、65%RH下で7日間養生してテストピース10個を作製し、そのうちの5個を使用してJIS K-6852に従って圧縮せん断強度を測定したところ、接着強度は118.3kg/cm2であり、使用したテストピースはすべて材料破壊した。また、残りのテストピース5個を30℃の水に3時間浸漬した後、同様にして圧縮せん断強度を測定したところ、接着強度は21.4kg/cm2であった。 [Wood adhesion test]
PVAc emulsion stabilized with Kuraray's “Poval” PVA-217 (7.5 parts of PVA-217 added to 100 parts of PVAc), the above-mentioned PVA14 was added, and the total solid content was 35%, 20 An aqueous emulsion adhesive containing 4 parts of phenoxyethanol with respect to 100 parts of PVAc having a viscosity of 10,000 mPa · s at 6 ° C. was prepared.
200 g / m 2 of the aqueous emulsion adhesive was applied to the rice husk material, and the same type of rice husk material was immediately bonded together and pressed at a pressure of 7 kg / cm 2 for 24 hours. Thereafter, the pressure was released and the test piece was cured for 7 days at 20 ° C. and 65% RH, and 10 test pieces were prepared. The compression shear strength was measured according to JIS K-6852 using 5 test pieces. 118.3 kg / cm 2 , and all the test pieces used were destroyed. Further, the remaining five test pieces were immersed in water at 30 ° C. for 3 hours, and then the compression shear strength was measured in the same manner. As a result, the adhesive strength was 21.4 kg / cm 2 .
得られた各PVAを用いて下記の方法で実施例33~48及び比較例17~24の紙用塗工剤を得た。得られた各紙用塗工剤を以下の方法にて評価した。評価結果を表3に示す。 Examples 33 to 48 and Comparative Examples 17 to 24 (paper coating agent)
Using the obtained PVA, paper coating agents for Examples 33 to 48 and Comparative Examples 17 to 24 were obtained by the following method. Each obtained paper coating agent was evaluated by the following methods. The evaluation results are shown in Table 3.
水酸化アルミニウム粉末(昭和電工社製、ハイジライトH42)90gを蒸留水210gに投入し、手動にて撹拌した。この後、ホモミキサー(IKA-Labortechnik社製、タイプT-25-SI)を用いて回転速度13,500rpmで5分間撹拌して、水酸化アルミニウムの分散液(水酸化アルミニウム濃度30%)を調製した。これとは別に、得られた各PVAを95℃の熱水に溶解させて、濃度4%のPVA水溶液を調製した。次に、PVA水溶液150gを上記水酸化アルミニウムの分散液20gに加え、両者を均一に混合した後、固形分濃度が4%となるように蒸留水を加えて塗工剤を得た。次に、塗工剤を、市販の感熱紙(コクヨ社製)の紙面に、ワイヤーバーのNo.60(ETO社製)を用いて手塗りした後、熱風乾燥機を用いて、塗工面を50℃で1時間乾燥させた。次に、乾燥後の感熱紙を、20℃、65%RHに調整した室内に3時間放置して、塗工剤により形成された感熱紙オーバーコート層の特性(耐水性、耐ブロッキング性)を評価するためのサンプルとした。 [Preparation of thermal paper overcoat layer]
90 g of aluminum hydroxide powder (manufactured by Showa Denko KK, Heidilite H42) was added to 210 g of distilled water and stirred manually. Thereafter, the mixture is stirred for 5 minutes at a rotational speed of 13,500 rpm using a homomixer (IKA-Labortechnik, type T-25-SI) to prepare an aluminum hydroxide dispersion (aluminum hydroxide concentration 30%). did. Separately, the obtained PVA was dissolved in 95 ° C. hot water to prepare a PVA aqueous solution having a concentration of 4%. Next, 150 g of PVA aqueous solution was added to 20 g of the above aluminum hydroxide dispersion, and both were uniformly mixed. Then, distilled water was added so that the solid concentration was 4% to obtain a coating agent. Next, the coating agent was applied to the surface of a commercially available thermal paper (manufactured by KOKUYO) with a wire bar No. After hand-painting using 60 (manufactured by ETO), the coated surface was dried at 50 ° C. for 1 hour using a hot air dryer. Next, the dried thermal paper is left in a room adjusted to 20 ° C. and 65% RH for 3 hours to determine the characteristics (water resistance and blocking resistance) of the thermal paper overcoat layer formed by the coating agent. It was set as the sample for evaluation.
上記サンプルを20℃の水に10分間浸漬させた後、塗工面を指で10回擦って、当該面に生じた剥がれの状態を観察した。塗工剤により形成された層の耐水性は、観察した状態を以下の基準により5段階で評価した。
耐水性の判定基準
5:表面の剥がれが全くなかった。
4:表面の剥がれがごく少しあった。
3:表面の剥がれが少しあった。
2:表面の剥がれが多かった。
1:表面の大部分が剥がれた。 [water resistant]
The sample was immersed in water at 20 ° C. for 10 minutes, and then the coated surface was rubbed 10 times with a finger to observe the state of peeling that occurred on the surface. The water resistance of the layer formed with the coating agent was evaluated in five stages according to the following criteria.
Criteria for water resistance 5: There was no peeling of the surface.
4: There was very little peeling of the surface.
3: There was some peeling of the surface.
2: There was much peeling of the surface.
1: Most of the surface was peeled off.
上記サンプルを40℃の雰囲気下に72時間放置した後、5cm角に裁断した。次に、塗工面に一滴(約30μL)の水を垂らした後、その上に、水滴を垂らしていない別のサンプルを塗工面同士が接触するように重ね、自然乾燥させた。乾燥後、サンプル同士を引き剥がして、その剥がれ方の状態を観察した。塗工剤により形成された層の耐ブロッキング性は、観察した状態を以下の基準により3段階で評価した。
耐ブロッキング性の判定基準
3:特に力を加えることなく、自然に離れた。
2:表面同士が部分的に付着していたが、サンプルに破れなどは生じなかった。
1:表面同士が付着しており、引き剥がしによってサンプルに破れが生じた。 [Blocking resistance (surface water resistance)]
The sample was allowed to stand in an atmosphere of 40 ° C. for 72 hours and then cut into 5 cm square. Next, after dropping one drop (about 30 μL) of water on the coated surfaces, another sample on which no water droplets were dropped was stacked on the coated surfaces so that the coated surfaces were in contact with each other and allowed to dry naturally. After drying, the samples were peeled apart to observe how they were peeled off. The blocking resistance of the layer formed with the coating agent was evaluated in three stages according to the following criteria based on the observed state.
Criteria for blocking resistance 3: Naturally separated without particular force.
2: The surfaces were partially adhered to each other, but the sample was not broken.
1: The surfaces were adhered to each other, and the sample was torn by peeling.
得られた各PVAについて固形分濃度4%の水溶液1,000gを調製し、該PVA水溶液を、気相法シリカ(アエロジルA300:日本アエロジル社製)の固形分濃度20%の分散液1,000gに加え、よく混合撹拌して分散液を得た。その後、蒸留水を添加して固形分濃度12質量%の塗工液(紙用塗工剤)を調製した。この塗工液の溶液粘度を、B型粘度計を用いてロータ回転数6rpm、温度20℃の条件で測定したところ、100mPa・sであった。コロナ処理を施したPETフィルムの表面に、メイヤーバーを用いて乾燥後の塗工量が15g/m2となるように30℃で上記塗工液を塗工し、熱風乾燥機にて150℃で3分間乾燥してインクジェット記録紙を製造した。 [Preparation of inkjet recording paper]
For each obtained PVA, 1,000 g of an aqueous solution having a solid content concentration of 4% was prepared, and the aqueous PVA solution was dispersed in a gaseous solution of silica (Aerosil A300: manufactured by Nippon Aerosil Co., Ltd.) at a solid content concentration of 20%, 1,000 g. In addition, the mixture was thoroughly mixed and stirred to obtain a dispersion. Thereafter, distilled water was added to prepare a coating liquid (paper coating agent) having a solid content concentration of 12% by mass. The solution viscosity of this coating solution was measured using a B-type viscometer under conditions of a rotor rotation speed of 6 rpm and a temperature of 20 ° C., and was 100 mPa · s. On the surface of the PET film subjected to corona treatment, the above coating solution is applied at 30 ° C. using a Mayer bar so that the coating amount after drying is 15 g / m 2, and 150 ° C. using a hot air dryer. And dried for 3 minutes to produce an ink jet recording paper.
上記方法により、インクジェット記録紙を製造し、そのインク受理層のひび割れを以下の基準で評価した。 [Evaluation of inkjet recording paper]
Ink jet recording paper was produced by the above method, and cracks of the ink receiving layer were evaluated according to the following criteria.
インク受理層の表面を光学顕微鏡により拡大倍率100倍で観察し、以下の基準により5段階で評価した。
5:表面にひび割れが全く観察されない。
4:表面にひび割れがほとんど観察されない。
3:表面に部分的にひび割れが発生。
2:表面に多数のひび割れが発生。
1:表面全体にひび割れが発生。 [crack]
The surface of the ink receiving layer was observed with an optical microscope at a magnification of 100 times, and was evaluated in five stages according to the following criteria.
5: No cracks are observed on the surface.
4: Almost no cracks are observed on the surface.
3: Cracks are partially generated on the surface.
2: Many cracks are generated on the surface.
1: Cracks occur on the entire surface.
坪量80g/m2、透気度140秒のセミグラシン紙に、濃度4%のPVA水溶液(紙用塗工剤)を、塗布量が0.1g/m2になるようMayerBarを用いて手塗り塗工し、110℃で1分間熱風乾燥機を用いて乾燥させた後に、20℃、65%RHで72時間調湿し、150℃、250Kg/cm、10m/分の条件でスーパーキャレンダー処理を1回実施した。得られた剥離紙原紙について、下記に示す方法で、透気度試験を実施した。 [Preparation of release paper base paper]
A semi-glassine paper with a basis weight of 80 g / m 2 and an air permeability of 140 seconds is hand-coated with a PVA aqueous solution (paper coating agent) with a concentration of 4% using a Mayer bar so that the coating amount is 0.1 g / m 2. After coating and drying at 110 ° C. for 1 minute using a hot air dryer, humidity was adjusted at 20 ° C. and 65% RH for 72 hours, and supercalender treatment was performed at 150 ° C., 250 Kg / cm, 10 m / min. Was performed once. About the obtained release paper base paper, the air permeability test was implemented by the method shown below.
JIS-P8117に準じて、王研式滑度透気度試験機を用いて剥離紙原紙の透気度を測定し、下記基準により5段階で評価した。
5:50,000秒以上
4:30,000秒以上、50,000秒未満
3:10,000秒以上、30,000秒未満
2: 1,000秒以上、10,000秒未満
1: 1,000秒未満 [Air permeability test of release paper base paper]
In accordance with JIS-P8117, the air permeability of the release paper base paper was measured using an Oken type lubricity air permeability tester, and evaluated in 5 stages according to the following criteria.
5: More than 50,000 seconds 4: 30,000 seconds or more, less than 50,000 seconds 3: 10,000 seconds or more, less than 30,000 seconds 2: 1,000 seconds or more, less than 10,000 seconds 1: 1, Less than 000 seconds
総合評価:上記4つの評価項目の合計得点から総合評価を実施し、その評価結果をPVAの性能評価としたところ、PVA1を用いたもの(実施例33)は15点となった。なお、この得点が10点以上のものを合格品、10点未満のものを不合格品と判定した。 [Comprehensive evaluation of paper coating agents]
Comprehensive evaluation: Comprehensive evaluation was performed from the total score of the above four evaluation items, and when the evaluation result was evaluated as PVA performance, the one using PVA1 (Example 33) was 15 points. In addition, the thing with this score of 10 points or more was determined to be an acceptable product if it was less than 10 points.
2)アルキル変性率/イタコン酸変性率
2) Alkyl modification rate / Itaconic acid modification rate
表4に記載の各PVA40部を、イオン交換水960部に常温で添加し、撹拌しながら1時間で95℃まで昇温した。95℃で2時間保持した後、撹拌しながら常温まで冷却し、4%のPVA水溶液をそれぞれ得た。 Examples 49-64 and Comparative Examples 25-32 (Adhesive)
40 parts of each PVA described in Table 4 was added to 960 parts of ion-exchanged water at room temperature, and the temperature was raised to 95 ° C. over 1 hour while stirring. After maintaining at 95 ° C. for 2 hours, the mixture was cooled to room temperature while stirring to obtain 4% PVA aqueous solution.
日本たばこ産業社製の初期接着試験機を用いて、以下の条件で初期接着力を測定した。
条件;クラフト紙/クラフト紙接着
塗布速度 0.5m/秒
せん断速度 300mm/秒
オープンタイム 1秒
圧着時間 2秒
養生時間 1秒、3秒、5秒、10秒
接着面積 1mm×25mm×8ヶ所(計2cm2)
温湿度 20℃、65%RH [Initial adhesion]
The initial adhesion strength was measured under the following conditions using an initial adhesion tester manufactured by Nippon Tobacco Inc.
Conditions: Kraft paper / craft paper adhesion Application speed 0.5m / sec Shear speed 300mm / sec Open time 1sec Crimping time 2sec Curing time 1sec, 3sec, 5sec, 10sec Adhesive area 1mm x 25mm x 8 locations ( 2cm 2 in total)
Temperature and humidity 20 ℃, 65% RH
接着剤を40℃で7日間放置した後の状態を観察し、保存前後の状態変化を以下の指標で評価した。
A;分離、沈降なく、粘度変化もなし。
B;分離、沈降がわずかに認められるが、流動性はあり。
C;分離、沈降が認められる。あるいは、流動性がない。 [Storage stability]
The state after the adhesive was allowed to stand at 40 ° C. for 7 days was observed, and the state change before and after storage was evaluated by the following indices.
A: No separation or sedimentation, no change in viscosity.
B: Slight separation and sedimentation are observed, but fluidity is present.
C: Separation and sedimentation are observed. Or there is no fluidity.
クラフト紙上に接着剤を固形分で10g/m2になるようにワイヤーバーを用いて塗工し、その上にクラフト紙を貼り付けた。このクラフト紙を20℃、65%RHで24時間養生した後に30℃の水に30秒間浸漬した。水を含んだクラフト紙の水分をろ紙を用いて軽くふき取った後に、接着層の180°剥離強度をオートグラフを用いて測定し、以下の指標で評価した。
A;クラフト紙の材破
B;1kg/cm2以上
C;1kg/cm2未満 [Water-resistant adhesion]
The adhesive was coated on the kraft paper with a wire bar so that the solid content was 10 g / m 2 , and the kraft paper was affixed thereon. The kraft paper was cured at 20 ° C. and 65% RH for 24 hours and then immersed in water at 30 ° C. for 30 seconds. The water of the kraft paper containing water was gently wiped off using a filter paper, and then the 180 ° peel strength of the adhesive layer was measured using an autograph and evaluated according to the following indicators.
A: Material breakage of kraft paper B: 1 kg / cm 2 or more C: Less than 1 kg / cm 2
2)アルキル変性率/イタコン酸変性率
2) Alkyl modification rate / Itaconic acid modification rate
実施例49で得られた4%のPVA1水溶液100部に対し、フィラーとしてクレー(Huber-900:カオリナイト系クレー、平均粒径0.6μm、Huber社製)8部を添加・撹拌し、クレーを十分分散させ、接着剤を調製した。該接着剤の固形分は12.0%、PVA1とクレーとの固形分質量比は100:200であった。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 65]
To 100 parts of the 4% PVA1 aqueous solution obtained in Example 49, 8 parts of clay (Huber-900: kaolinite clay, average particle size 0.6 μm, manufactured by Huber) as a filler was added and stirred. Was sufficiently dispersed to prepare an adhesive. The solid content of the adhesive was 12.0%, and the solid content mass ratio of PVA1 to clay was 100: 200. Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
PVA1水溶液に代えて、実施例64で得られたPVA16水溶液を用いた以外は実施例65と同様にクレーを添加し、接着剤を調製した。該接着剤の固形分は12.0%、PVA16とクレーの固形分質量比は100:200であった。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 73]
Instead of the PVA1 aqueous solution, clay was added in the same manner as in Example 65 except that the PVA16 aqueous solution obtained in Example 64 was used to prepare an adhesive. The solid content of the adhesive was 12.0%, and the solid content mass ratio of PVA16 and clay was 100: 200. Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
PVA1水溶液に代えて、比較例32で得られたPVAviii水溶液を用いた以外は実施例65と同様にクレーを添加し、接着剤を調製した。該接着剤の固形分は12.0%、PVAviiiとクレーの固形分質量比は100:200であった。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Comparative Example 33]
Clay was added in the same manner as in Example 65 except that the PVAviii aqueous solution obtained in Comparative Example 32 was used in place of the PVA1 aqueous solution to prepare an adhesive. The solid content of the adhesive was 12.0%, and the mass ratio of the solid content of PVAviii and clay was 100: 200. Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
還流冷却器、滴下ロート、温度計、窒素吹込口及びイカリ型撹拌翼を備えたガラス製重合容器に、イオン交換水450部とPVA-117(クラレ社製)を32部仕込み、95℃で溶解した。次に、このPVA-117水溶液を冷却、窒素置換後、140rpmで撹拌しながら酢酸ビニル40部を仕込み、60℃に昇温した後、過酸化水素/酒石酸のレドックス開始剤系の存在下で重合を開始した。重合開始15分後から酢酸ビニル360部を3時間にわたって連続的に添加し、重合を完結させて、酢酸ビニル重合体(PVAc)のエマルジョンを得た。使用した開始剤は、1%過酸化水素水30g、5%酒石酸水溶液10gであった。得られたPVAcエマルジョンの固形分濃度は46.8%であった。実施例49で得られた4%のPVA1水溶液100部とPVAcエマルジョン34.1部とを混合し接着剤を調製した(PVA1とPVAcの固形分質量比は100:400)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 66]
In a glass polymerization vessel equipped with a reflux condenser, dropping funnel, thermometer, nitrogen inlet, and squid type stirring blade, 450 parts of ion-exchanged water and 32 parts of PVA-117 (manufactured by Kuraray Co., Ltd.) were charged and dissolved at 95 ° C. did. Next, the PVA-117 aqueous solution was cooled, purged with nitrogen, charged with 40 parts of vinyl acetate while stirring at 140 rpm, heated to 60 ° C., and then polymerized in the presence of a redox initiator system of hydrogen peroxide / tartaric acid. Started. From 15 minutes after the start of polymerization, 360 parts of vinyl acetate was continuously added over 3 hours to complete the polymerization, and an emulsion of vinyl acetate polymer (PVAc) was obtained. The initiator used was 30 g of 1% hydrogen peroxide solution and 10 g of 5% aqueous tartaric acid solution. The solid content concentration of the obtained PVAc emulsion was 46.8%. An adhesive was prepared by mixing 100 parts of the 4% PVA1 aqueous solution obtained in Example 49 and 34.1 parts of PVAc emulsion (solid content mass ratio of PVA1 and PVAc was 100: 400). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
PVA1水溶液に代えて、実施例64で得られたPVA16水溶液を用いた以外は実施例66と同様の操作を行い、接着剤を調製した(PVA16とPVAcの固形分質量比は100:400)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 74]
An adhesive was prepared in the same manner as in Example 66 except that the PVA16 aqueous solution obtained in Example 64 was used instead of the PVA1 aqueous solution (the solid content mass ratio of PVA16 and PVAc was 100: 400). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
PVA1水溶液に代えて、比較例32で得られたPVAviii水溶液を用いた以外は実施例66と同様の操作を行い、接着剤を調製した(PVAviiiとPVAcの固形分質量比は100:400)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Comparative Example 34]
An adhesive was prepared in the same manner as in Example 66 except that the PVAviii aqueous solution obtained in Comparative Example 32 was used instead of the PVA1 aqueous solution (the solid mass ratio of PVAviii and PVAc was 100: 400). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
実施例49で得られたPVA1水溶液100部にクレー(Huber-900:カオリナイト系クレー、平均粒径0.6μm、Huber社製)8部を添加・撹拌し、クレーを十分分散させた。この分散液に実施例66で得られたPVAcエマルジョン34.1部を添加混合し、接着剤を調製した(PVA1とPVAcとクレーの固形分質量比は100:400:200)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 67]
To 100 parts of the PVA1 aqueous solution obtained in Example 49, 8 parts of clay (Huber-900: kaolinite clay, average particle size 0.6 μm, manufactured by Huber) was added and stirred to sufficiently disperse the clay. To this dispersion, 34.1 parts of the PVAc emulsion obtained in Example 66 was added and mixed to prepare an adhesive (the solid content mass ratio of PVA1, PVAc, and clay was 100: 400: 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
PVA1水溶液に代えて、実施例64で得られたPVA16水溶液を用いた以外は実施例67と同様の操作を行い、接着剤を調製した(PVA16とPVAcとクレーの固形分質量比は100:400:200)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 75]
An adhesive was prepared in the same manner as in Example 67 except that the PVA16 aqueous solution obtained in Example 64 was used instead of the PVA1 aqueous solution (the solid mass ratio of PVA16, PVAc, and clay was 100: 400). : 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
PVA1水溶液に代えて、比較例32で得られたPVAviii水溶液を用いた以外は実施例67と同様の操作を行い、接着剤を調製した(PVAviiiとPVAcとクレーの固形分質量比は100:400:200)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Comparative Example 35]
An adhesive was prepared in the same manner as in Example 67 except that the PVAviii aqueous solution obtained in Comparative Example 32 was used instead of the PVA1 aqueous solution (the solid mass ratio of PVAviii, PVAc, and clay was 100: 400). : 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
クレーに代えて、炭酸カルシウム(ホワイトンP-30、重質炭酸カルシウム、平均粒径1.75μm、白石工業社製)又は酸化澱粉(MS-3800、日本食品加工製)をそれぞれ用いた以外は実施例67と同様の操作を行い、接着剤をそれぞれ得た。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Examples 68 and 69]
Instead of clay, calcium carbonate (Whiteon P-30, heavy calcium carbonate, average particle size 1.75 μm, manufactured by Shiroishi Kogyo Co., Ltd.) or oxidized starch (MS-3800, manufactured by Nippon Food Processing) was used. The same operations as in Example 67 were performed to obtain adhesives. Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
還流冷却器、滴下ロート、温度計及び窒素吹込口を備えたガラス製重合容器に、イオン交換水500部、末端にメルカプト基を有するポリビニルアルコール(M-205:重合度550、けん化度88.2モル%、クラレ社製)28部を仕込み、95℃で溶解した。次に、メタクリル酸メチル20gとアクリル酸n-ブチル20gとを添加し、窒素置換後65℃まで昇温し、1%過硫酸カリウム水溶液12gを添加して重合を開始し、さらに2時間かけてメタクリル酸メチル180g、アクリル酸n-ブチル180gを連続的に添加した。重合は4時間で完結し、固形分濃度45.1%、粘度2800mPa・sのメタクリル酸メチル/アクリル酸n-ブチル共重合体(ACR)エマルジョンを得た。実施例49で得られたPVA1水溶液100部にクレー(Huber-900:カオリナイト系クレー、平均粒径0.6μm、Huber社製)8部を添加・撹拌し、クレーを十分分散させ、それにACRエマルジョン35.4部を添加混合し接着剤を調製した(PVA1とACRとクレーの固形分質量比は100:400:200)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 70]
In a glass polymerization vessel equipped with a reflux condenser, a dropping funnel, a thermometer and a nitrogen inlet, 500 parts of ion-exchanged water and polyvinyl alcohol having a mercapto group at the end (M-205: polymerization degree 550, saponification degree 88.2). (Mole%, manufactured by Kuraray Co., Ltd.) 28 parts were charged and dissolved at 95 ° C. Next, 20 g of methyl methacrylate and 20 g of n-butyl acrylate were added, the temperature was raised to 65 ° C. after nitrogen substitution, and 12 g of a 1% aqueous potassium persulfate solution was added to initiate the polymerization. 180 g of methyl methacrylate and 180 g of n-butyl acrylate were continuously added. The polymerization was completed in 4 hours to obtain a methyl methacrylate / n-butyl acrylate copolymer (ACR) emulsion having a solid content concentration of 45.1% and a viscosity of 2800 mPa · s. To 100 parts of the PVA1 aqueous solution obtained in Example 49, 8 parts of clay (Huber-900: kaolinite-based clay, average particle size 0.6 μm, manufactured by Huber) was added and stirred to sufficiently disperse the clay. 35.4 parts of the emulsion was added and mixed to prepare an adhesive (PVA1, ACR and clay solid mass ratio of 100: 400: 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
メタクリル酸メチル/アクリル酸n-ブチル共重合体(ACR)エマルジョンに代えて、エチレン-酢酸ビニル共重合体(VAE)エマルジョン(OM-4200NT、固形分濃度55.0%、クラレ社製)を29.0部用いた以外は実施例70と同様の操作を行い、接着剤を調製した(PVA1とVAEとクレーの固形分質量比は100:400:200)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 71]
In place of the methyl methacrylate / n-butyl acrylate copolymer (ACR) emulsion, 29 ethylene-vinyl acetate copolymer (VAE) emulsion (OM-4200NT, solid content concentration 55.0%, manufactured by Kuraray Co., Ltd.) An adhesive was prepared in the same manner as in Example 70 except that 0.0 part was used (the solid content mass ratio of PVA1, VAE and clay was 100: 400: 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
メタクリル酸メチル/アクリル酸n-ブチル共重合体(ACR)エマルジョンに代えて、スチレン-ブタジエン共重合体(SBR)エマルジョン(ナルスターSR-107、固形分濃度48.0%、日本エイアンドエル社製)を33.3部用いた以外は実施例70と同様の操作を行い、接着剤を調製した(PVA1とSBRとクレーの固形分質量比は100:400:200)。これを用い、上記方法に従い、初期接着性、保存安定性及び耐水接着性の評価を行った。結果を表5に示す。 [Example 72]
Instead of methyl methacrylate / n-butyl acrylate copolymer (ACR) emulsion, styrene-butadiene copolymer (SBR) emulsion (Nalstar SR-107, solid content concentration 48.0%, manufactured by Nippon A & L Co., Ltd.) The same operation as in Example 70 was performed except that 33.3 parts were used to prepare an adhesive (the solid content mass ratio of PVA1, SBR, and clay was 100: 400: 200). Using this, according to the said method, initial adhesiveness, storage stability, and water-resistant adhesiveness were evaluated. The results are shown in Table 5.
上記PVAの水溶性の試験と同様にして、表6に記載の各PVAを用い、濃度4%のPVA水溶液をそれぞれ調製した。各PVA水溶液をPETフィルム上に流延した後、20℃、65%RHの条件下で1週間乾燥させ、実施例76~90及び比較例36~43のPVAフィルムをそれぞれ得た。各PVAフィルムの厚みは100μmであった。得られた各フィルムについて、以下の方法にて評価した。評価結果を表6に示す。 Examples 76 to 90 and Comparative Examples 36 to 43 (film)
In the same manner as the water solubility test of PVA, PVA aqueous solutions having a concentration of 4% were prepared using the PVA listed in Table 6. Each PVA aqueous solution was cast on a PET film and then dried for 1 week under the conditions of 20 ° C. and 65% RH to obtain PVA films of Examples 76 to 90 and Comparative Examples 36 to 43, respectively. The thickness of each PVA film was 100 μm. Each obtained film was evaluated by the following methods. The evaluation results are shown in Table 6.
得られたPVAフィルムの触感を、クラレ社製「PVA-117」を用いて同様に製造したフィルムと比較し、以下の基準で判定した。
A:PVA-117と同様にしなやか
B:PVA-117より少し硬くもろい
C:PVA-117よりも著しく硬くもろい [Feel of film]
The tactile sensation of the obtained PVA film was compared with a film produced in the same manner using “PVA-117” manufactured by Kuraray Co., Ltd., and judged according to the following criteria.
A: Flexible as in PVA-117 B: Slightly harder and brittle than PVA-117 C: Remarkably harder and brittle than PVA-117
得られたPVAフィルムの接触角を、協和界面科学社製固液界面解析装置 DropMaster500を用いて測定し、以下の基準で判定した。
A:90°以上
B:85°以上90°未満
C:80°以上85°未満
D:70°以上80°未満
E:70°未満 [Measurement of film contact angle]
The contact angle of the obtained PVA film was measured using a solid-liquid interface analyzer DropMaster500 manufactured by Kyowa Interface Science Co., Ltd., and judged according to the following criteria.
A: 90 ° or more B: 85 ° or more and less than 90 ° C: 80 ° or more and less than 85 ° D: 70 ° or more and less than 80 ° E: Less than 70 °
2)アルキル変性率/イタコン酸変性率
2) Alkyl modification rate / Itaconic acid modification rate
Claims (17)
- 下記一般式(I)で表される単量体単位(a)を含有し、粘度平均重合度が200以上5,000以下、けん化度が20モル%以上99.99モル%以下、上記単量体単位(a)の含有率が0.05モル%以上5モル%以下であるアルキル変性ビニルアルコール系重合体。
- 上記式(I)におけるR1が、炭素数15~26の直鎖状又は分岐状アルキル基である請求項1に記載のアルキル変性ビニルアルコール系重合体。 2. The alkyl-modified vinyl alcohol polymer according to claim 1, wherein R 1 in the formula (I) is a linear or branched alkyl group having 15 to 26 carbon atoms.
- けん化度が60モル%以上99.9モル%以下である請求項1又は請求項2に記載のアルキル変性ビニルアルコール系重合体。 The alkyl-modified vinyl alcohol polymer according to claim 1 or 2, wherein the saponification degree is 60 mol% or more and 99.9 mol% or less.
- 下記一般式(II)で表される不飽和単量体とビニルエステル系単量体との共重合体をけん化することにより得られたものである請求項1、請求項2又は請求項3に記載のアルキル変性ビニルアルコール系重合体。
- カルボキシル基を有する単量体単位(b)の含有率が0.1モル%未満である請求項1から請求項4のいずれか1項に記載のアルキル変性ビニルアルコール系重合体。 The alkyl-modified vinyl alcohol polymer according to any one of claims 1 to 4, wherein the content of the monomer unit (b) having a carboxyl group is less than 0.1 mol%.
- 請求項1から請求項5のいずれか1項に記載のアルキル変性ビニルアルコール系重合体を含む組成物。 A composition comprising the alkyl-modified vinyl alcohol polymer according to any one of claims 1 to 5.
- 水及び油分をさらに含み、この油分100質量部に対する上記アルキル変性ビニルアルコール系重合体の含有量が0.1質量部以上50質量部以下である請求項6に記載の組成物。 The composition according to claim 6, further comprising water and an oil, wherein the content of the alkyl-modified vinyl alcohol polymer with respect to 100 parts by mass of the oil is 0.1 parts by mass or more and 50 parts by mass or less.
- 請求項1から請求項5のいずれか1項に記載のアルキル変性ビニルアルコール系重合体を含む増粘剤。 A thickener comprising the alkyl-modified vinyl alcohol polymer according to any one of claims 1 to 5.
- 水又は水含有溶媒をさらに含む請求項8に記載の増粘剤。 The thickener according to claim 8, further comprising water or a water-containing solvent.
- 請求項1から請求項5のいずれか1項に記載のアルキル変性ビニルアルコール系重合体を含む紙用塗工剤。 A paper coating agent comprising the alkyl-modified vinyl alcohol polymer according to any one of claims 1 to 5.
- 請求項10に記載の紙用塗工剤が紙表面に塗工されてなる塗工紙。 A coated paper obtained by coating the paper coating agent according to claim 10 on the paper surface.
- 請求項1から請求項5のいずれか1項に記載のアルキル変性ビニルアルコール系重合体を含む接着剤。 An adhesive comprising the alkyl-modified vinyl alcohol polymer according to any one of claims 1 to 5.
- エチレン系不飽和単量体及びジエン系単量体からなる群より選ばれる少なくとも1種の単量体から得られる重合体をエマルジョン状態でさらに含む請求項12に記載の接着剤。 The adhesive according to claim 12, further comprising, in an emulsion state, a polymer obtained from at least one monomer selected from the group consisting of an ethylenically unsaturated monomer and a diene monomer.
- フィラーをさらに含む請求項12又は請求項13に記載の接着剤。 The adhesive according to claim 12 or 13, further comprising a filler.
- 紙用又は木工用である請求項12、請求項13又は請求項14に記載の接着剤。 The adhesive according to claim 12, 13 or 14, which is for paper or woodwork.
- 請求項1から請求項5のいずれか1項に記載のアルキル変性ビニルアルコール系重合体を含むフィルム。 A film comprising the alkyl-modified vinyl alcohol polymer according to any one of claims 1 to 5.
- 水との接触角が70°以上である請求項16に記載のフィルム。
The film according to claim 16, which has a contact angle with water of 70 ° or more.
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US13/703,140 US9156928B2 (en) | 2010-06-09 | 2011-06-08 | Alkyl-modified vinyl alcohol polymer, and composition, thickener, coating material for paper, coated paper, adhesive and film containing the same |
EP11792503.2A EP2581393B1 (en) | 2010-06-09 | 2011-06-08 | Alkyl-modified vinyl alcohol polymer, and composition, thickener, coating material for paper, coated paper, adhesive and film containing the same |
CN201180028206.XA CN102958954B (en) | 2010-06-09 | 2011-06-08 | Alkyl-modified vinyl alcohol system polymer and containing its composition, tackifier, paper coating agent, White Board, caking agent and film |
KR1020137000103A KR101790377B1 (en) | 2010-06-09 | 2011-06-08 | Alkyl-modified vinyl alcohol polymer, and composition, thickener, coating material for paper, coated paper, adhesive and film that contain same |
ES11792503.2T ES2687704T3 (en) | 2010-06-09 | 2011-06-08 | Alkyl modified vinyl alcohol polymer, and composition, thickener, paper coating material, coated paper, adhesive and film containing it |
JP2012519422A JP5813635B2 (en) | 2010-06-09 | 2011-06-08 | Alkyl-modified vinyl alcohol polymer, composition containing the same, thickener, paper coating agent, coated paper, adhesive and film |
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EP2581393B1 (en) | 2018-08-08 |
US20130209817A1 (en) | 2013-08-15 |
KR101790377B1 (en) | 2017-10-25 |
EP2581393A4 (en) | 2014-12-31 |
EP2581393A1 (en) | 2013-04-17 |
ES2687704T3 (en) | 2018-10-26 |
MY160895A (en) | 2017-03-31 |
JP5813635B2 (en) | 2015-11-17 |
US9156928B2 (en) | 2015-10-13 |
CN102958954A (en) | 2013-03-06 |
KR20130098978A (en) | 2013-09-05 |
JPWO2011155546A1 (en) | 2013-08-01 |
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